CN103468848B - Method for treating high-iron red mud by high-temperature iron bath - Google Patents
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- CN103468848B CN103468848B CN201310402154.9A CN201310402154A CN103468848B CN 103468848 B CN103468848 B CN 103468848B CN 201310402154 A CN201310402154 A CN 201310402154A CN 103468848 B CN103468848 B CN 103468848B
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 181
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 86
- 238000000034 method Methods 0.000 title claims abstract description 47
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 19
- 239000002893 slag Substances 0.000 claims abstract description 16
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 12
- 239000012535 impurity Substances 0.000 claims abstract description 10
- 238000009628 steelmaking Methods 0.000 claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 9
- 239000000654 additive Substances 0.000 claims abstract description 8
- 230000000996 additive effect Effects 0.000 claims abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 8
- 239000001301 oxygen Substances 0.000 claims abstract description 8
- 230000009467 reduction Effects 0.000 claims abstract description 8
- 230000009471 action Effects 0.000 claims abstract description 6
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims abstract description 6
- 239000000428 dust Substances 0.000 claims abstract description 5
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 4
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 3
- 238000010079 rubber tapping Methods 0.000 claims abstract 2
- YOBAEOGBNPPUQV-UHFFFAOYSA-N iron;trihydrate Chemical compound O.O.O.[Fe].[Fe] YOBAEOGBNPPUQV-UHFFFAOYSA-N 0.000 claims description 37
- 230000008569 process Effects 0.000 claims description 19
- 239000010436 fluorite Substances 0.000 claims description 11
- 239000000843 powder Substances 0.000 claims description 11
- 239000002817 coal dust Substances 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 10
- 238000001035 drying Methods 0.000 claims description 8
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 7
- 229910052708 sodium Inorganic materials 0.000 claims description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 5
- 239000005864 Sulphur Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 238000005266 casting Methods 0.000 claims description 4
- 239000003500 flue dust Substances 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 229910004261 CaF 2 Inorganic materials 0.000 claims description 2
- 238000005054 agglomeration Methods 0.000 claims description 2
- 230000002776 aggregation Effects 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 6
- 229910052751 metal Inorganic materials 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000002844 melting Methods 0.000 abstract description 2
- 230000008018 melting Effects 0.000 abstract description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 abstract 2
- 238000004134 energy conservation Methods 0.000 abstract 1
- 150000002739 metals Chemical class 0.000 abstract 1
- 239000000779 smoke Substances 0.000 abstract 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 abstract 1
- 229910001948 sodium oxide Inorganic materials 0.000 abstract 1
- 238000006722 reduction reaction Methods 0.000 description 9
- 239000011734 sodium Substances 0.000 description 7
- 239000004411 aluminium Substances 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 4
- 229910052728 basic metal Inorganic materials 0.000 description 3
- 150000003818 basic metals Chemical class 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000007885 magnetic separation Methods 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 238000005453 pelletization Methods 0.000 description 3
- 238000012797 qualification Methods 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 241000450840 Tropheops sp. 'red' Species 0.000 description 2
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000011499 joint compound Substances 0.000 description 2
- 230000005415 magnetization Effects 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 238000004131 Bayer process Methods 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- CYUOWZRAOZFACA-UHFFFAOYSA-N aluminum iron Chemical compound [Al].[Fe] CYUOWZRAOZFACA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000007600 charging Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention provides a method for treating high-iron red mud by using a high-temperature iron bath, which comprises the steps of uniformly mixing high-iron red mud, a carbon-containing raw material and an additive according to the proportion that the additive accounts for 4-10wt%, the mole ratio of the fixed carbon content in the carbon-containing raw material to the total oxygen content of iron oxide and sodium oxide in the high-iron red mud is C/O = 1.1-1.4, and preparing red mud briquettes; when tapping the iron from the blast furnace, adding the molten iron according to the addition amount of less than or equal to 50 kg/t, and rapidly melting and reducing the metals in the red mud by utilizing the high-temperature iron bath environment and the impact and stirring action of the molten iron; the iron is reduced and melted in high-temperature molten iron for steel making, the alkali metal is reduced and then discharged along with smoke dust, and aluminum oxide and impurities are melted in slag and float on the surface of the molten iron. The method is simple and easy to implement, does not need to increase special devices or equipment, can efficiently separate iron, aluminum and alkali metals in the red mud, has the iron recovery rate of over 90 percent, not only realizes large-scale comprehensive utilization of the high-iron red mud, but also alleviates the environmental and safety problems caused by the red mud, and obtains the double effects of energy conservation and emission reduction.
Description
Technical field
The invention belongs to metallurgical comprehensive and utilize field, be specifically related to a kind of method utilizing high temperature iron to bathe process iron red mud.
Background technology
Red mud is the solid waste that alumina producer produces alumina process China and foreign countries row, general 1t aluminum oxide of often producing about produces 0.8 ~ 1.8t red mud, its comprehensive utilization ratio is very low, the red mud storage of current China is accumulative reaches more than 200,000,000 ton, both take a large amount of soil, cause again environmental pollution and potential safety hazard.Containing the more valuable element such as iron, aluminium in red mud, after especially adopting alumina producing Bayer process, the red mud of outer row, generally has higher iron level (Fe
2o
3content 30% ~ 70%), thus the recycling of this iron red mud is worth high, and first-selection is the iron reclaimed wherein, and effectively process iron red mud not only alleviates environmental protection pressure but also can obtain economic benefit.But because the basic metal such as sodium in iron red mud and alumina content exceed standard, generally can not be directly used in conventional blast furnace ironmaking, still can not utilize in a large number in the industrial production at present.
In existing iron red mud treatment process, mainly mode such as employing reducing roasting and magnetic separation etc. reclaims iron wherein, such as Chinese patent CN102839249A " a kind of rotary hearth furnace direct-reduction iron red mud produces the method for Iron concentrate ", CN102628097A " a kind of fluid bed reduction magnetization treatment red mud prepares the method for Iron concentrate ", CN102626670A " a kind of rotary kiln reduction magnetization process red mud prepares the method for Iron concentrate " etc. adopt rotary hearth furnace, fluidized-bed, rotary kiln etc. to carry out reducing roasting for main technique to red mud respectively, then carry out magnetic separation to reclaim iron.CN102851425A " method of a kind of iron red mud iron, aluminium, sodium high efficiency separation comprehensive utilization " first uses rotary hearth furnace direct-reduction to carry out slag sluicing system to reclaim iron through peroxide coal iron bath fusion stove again.CN102816880A " method of aluminium comprehensive utilization is put forward in a kind of iron red mud ironmaking " adopts blast furnace to be main technique, require that red mud prepares mini-pellets composite sinter or pellet, then itself and coke are entered blast furnace being not less than 400 DEG C of temperature lower leaf hot chargings, adopts super oxygen even total oxygen air blast carry out the method recovery iron smelted.The multiple technologies such as CN102134646A " with Aluminum iron red mud for the method for metallic iron and aluminium concentrate directly prepared by raw material " adopts the meticulous reduction technique of Ultrafine Grinding technology, CO, non-melt is separated, first reduce and carry out magnetic separation again and reclaim iron.In addition, also adopt the reducing process such as rotary hearth furnace that red mud is reduced into sponge iron or granulated iron etc. to reclaim iron etc. just like some patents such as CN102329911A " technique of manufacturing iron pellets from low-grade complex refractory ore through molten slag method ".
In current iron red mud treatment process, mostly need to increase special arrangement or equipment, process is many, causes complex operation; Or control condition is strict, energy consumption is high, the rate of recovery is low, causes cost to increase, and is difficult to realize industrial production large-scale application.
Summary of the invention
The present invention aims to provide a kind of without the need to increasing special arrangement or equipment, utilize traditional blast furnace iron-making process, just can realize low cost, simple and effective is separated iron, aluminium, basic metal in iron red mud, and directly reclaim and utilize the high temperature iron bath of wherein iron resources to process the method for iron red mud.
For this reason, the solution that the present invention takes is:
A method for high temperature iron bath process iron red mud, its concrete steps are:
1, prepare burden:
Iron red mud, carbon raw material and additive are prepared burden according to the ratio that the oxygen element total content mol ratio of ferriferous oxide, na oxide in fixed carbon content in additive 4-10wt%, carbon raw material and iron red mud used is C/O=1.1 ~ 1.4, and mixes;
2, agglomeration:
Ball press or pelletizer is used to make the red mud agglomerate of diameter 5-40mm, drying for standby the compound after mixing;
3, high temperature iron bath:
Before blast furnace casting or tap a blast furnace process time, the add-on that the red mud agglomerate of drying is no more than 50 kg by molten iron per ton is joined in iron ladle or molten iron, utilizes high temperature iron to bathe impact, the stirring action of environment and molten iron, red mud agglomerate Flashmelt is reduced; Be fused to high temperature liquid iron after Fe3+ reduction in red mud agglomerate, supply follow-up steel-making by normal operation; Discharge with flue dust volatilization after alkali metal reduction, focused on by dust removal installation; Aluminum oxide and impurity are fused to slag and float over molten iron surface, focus on to the desulphurization and slag skimming of steel-making work area by normal operation.
The main chemical compositions of described iron red mud is: Fe
2o
3be 30 ~ 70 wt%, Al
2o
3be 5 ~ 30 wt%, Na
2o is 0 ~ 10 wt%, and all the other are SiO
2, CaO and other impurity.
Described carbon raw material is coal dust or coke powder, and its fixed carbon content is greater than 70wt%, and sulphur content is less than 1wt%.
Described additive is Fluorspar Powder, its CaF
2content>=85 wt%.
The feed postition of described red mud agglomerate for add molten iron stream from trough, swinging flow jet continuous uniform, or joins in iron ladle slack tank in advance, and then loads molten iron.
Beneficial effect of the present invention is:
1. the inventive method process flow is short, simple and easy to do, and not needing increases special arrangement or equipment, all utilizes iron and steel enterprise's existing device, does not affect normal operation system simultaneously;
2. the inventive method makes full use of the heat of high temperature liquid iron and impact, stirring action, good thermodynamic condition and dynamic conditions is provided for red mud agglomerate carries out iron-bath molten reduction reaction, can iron, aluminium, basic metal in high efficiency separation red mud, wherein the rate of recovery of iron reaches more than 90%, and can directly for steel-making;
3. the inventive method can realize the large-scale comprehensive utilization of iron red mud, can not only alleviate environment, safety problem that red mud causes, the iron resources that recoverable is a large amount of again, thus the double effects simultaneously obtaining energy-saving and emission-reduction.
Embodiment
Embodiment 1:
The chemical composition of iron red mud is mainly: Fe
2o
3be 65.2 wt%, Al
2o
3be 8.1 wt%, Na
2o is 2.4 wt%, and all the other are SiO
2, other impurity such as CaO.The fixed carbon content of coal dust is 72.1 wt%, and sulphur content is 0.8 wt%; The CaF of Fluorspar Powder
2content is 85.9 wt%.
Use mixer that iron red mud, coal dust, Fluorspar Powder are mixed in proportion and are stirred, wherein the proportioning of Fluorspar Powder is 5.0 wt%, all the other are iron red mud and coal dust, and in the fixed carbon content in coal dust and iron red mud, the oxygen element total content mol ratio of ferriferous oxide, na oxide is C/O=1.1.Then ball press is used to make 20 ~ 40mm red mud agglomerate, drying for standby.
In blast furnace casting process, use chute to add in trough by the red mud agglomerate continuous uniform of drying, add-on is 50kg/t.Red mud agglomerate falls into iron ladle with molten iron stream, and under the high temperature iron bath environment of about 1500 DEG C and molten iron fall the impact of formation, stirring action, red mud agglomerate Flashmelt reduces, and ferriferous oxide is reduced into metallic iron and is fused to molten iron; Alkalimetal oxide is reduced into lower boiling simple substance and discharges with flue dust volatilization, is focused on by dust removal installation; Aluminum oxide and other impurity are fused to slag and float over molten iron surface, focus on, the follow-up steel-making of hot metal supply by normal operation to steel-making work area desulphurization and slag skimming.
Before red mud agglomerate and desulfurization, the some chemical properties of slag is in table 1 and table 2.
Table 1. red mud agglomerate some chemical properties wt%
| TFe | Na 2O | C | F - | MgO | Al 2O 3 | SiO 2 | TCa | S | MnO |
| 32.91 | 1.68 | 16.81 | 2.02 | 0.67 | 6.65 | 3.95 | 3.51 | 0.15 | 0.31 |
Slag some chemical properties wt% before table 2. desulfurization
| TFe | F - | MgO | Al 2O 3 | SiO 2 | TCa | S | MnO |
| 3.25 | 3.06 | 5.56 | 7.68 | 57.65 | 10.86 | 0.21 | 4.67 |
According to the material balance relationship of Fe, calculate by agglomerate add-on 50kg/t, the quantity of slag that agglomerate is formed should be less than 28.5kg/t(and consider that the quantity of slag is with by molten iron 0.5%), in slag, TFe quality is less than 0.93kg/t, and TFe quality is 16.5kg/t in agglomerate, under can calculating these technical qualification, iron yield is greater than 94.4%.
Embodiment 2:
The chemical composition of iron red mud is mainly: Fe
2o
3be 51.5 wt%, Al
2o
3be 18.0 wt%, Na
2o is 8.2 wt%, and all the other are SiO
2, other impurity such as CaO; The fixed carbon content of coal dust is 71.6 wt%, and sulphur content is 0.8 wt%; The CaF of Fluorspar Powder
2content is 90.2 wt %.
Use mixer that iron red mud, coal dust, Fluorspar Powder are mixed in proportion and are stirred, then use pelletizer to make 5 ~ 10mm red mud pelletizing, drying for standby.Wherein the proportioning of Fluorspar Powder is 6.5 wt%, and all the other are iron red mud and coal dust, and in the fixed carbon content in coal dust and iron red mud, the oxygen element total content mol ratio of ferriferous oxide, na oxide is C/O=1.2.
10t red mud pelletizing is added in advance in the fish torpedo ladle slack tank (dress iron water amount 230t) having rolled over iron, molten iron is loaded when blast furnace casting, the impact of formation is fallen at the high temperature iron bath environment of about 1500 DEG C and molten iron, under stirring action, red mud pelletizing melting and reducing fast, ferriferous oxide is reduced into metallic iron and is fused to molten iron, alkalimetal oxide is reduced into lower boiling simple substance and discharges with flue dust volatilization, focused on by dust removal installation, aluminum oxide and other impurity are fused to slag and float over molten iron surface, focus on to steel-making work area desulphurization and slag skimming by normal operation, the follow-up steel-making of hot metal supply.
Detect through sampling and analyze, under these technical qualification, the rate of recovery of Fe is 91.1%.
Embodiment 3:
The chemical composition of iron red mud is mainly: Fe
2o
3be 36.5 wt%, Al
2o
3be 25.5 wt%, Na
2o is 9.3 wt%, and all the other are SiO
2, other impurity such as CaO; The fixed carbon content of coke powder is 82.4 wt%, and sulphur content is 0.6 wt%; The CaF of Fluorspar Powder
2content is 95.7 wt%.
Use mixer that iron red mud, coke powder, Fluorspar Powder are mixed in proportion and are stirred, then use ball press to make 10 ~ 30mm red mud agglomerate, drying for standby.Wherein the proportioning of Fluorspar Powder is 9.5 wt%, and all the other are iron red mud and coke powder, and in the fixed carbon content in coke powder and iron red mud, the oxygen element total content mol ratio of ferriferous oxide, na oxide is C/O=1.4.
Red mud agglomerate adds from swinging flow jet, and add-on is 40kg/t.Red mud agglomerate falls into iron ladle with molten iron stream, and other technique is identical with embodiment 1.
Detect through sampling and analyze, under these technical qualification, the rate of recovery of Fe is 96.3%.
Claims (5)
1. a method for high temperature iron bath process iron red mud, it is characterized in that, concrete steps are:
(1), prepare burden:
Iron red mud, carbon raw material and additive are prepared burden according to the ratio that the oxygen element total content mol ratio of ferriferous oxide, na oxide in fixed carbon content in additive 4-10wt%, carbon raw material and iron red mud used is C/O=1.1 ~ 1.4, and mixes;
(2), agglomeration:
Ball press or pelletizer is used to make the red mud agglomerate of diameter 5-40mm, drying for standby the compound after mixing;
(3), high temperature iron bath:
Before blast furnace casting or when tapping a blast furnace, the add-on that the red mud agglomerate of drying is no more than 50kg by molten iron per ton is joined in iron ladle or molten iron, utilize high temperature iron to bathe impact, the stirring action of environment and molten iron, red mud agglomerate Flashmelt is reduced; Be fused to high temperature liquid iron after Fe3+ reduction in red mud agglomerate, supply follow-up steel-making by normal operation; Discharge with flue dust volatilization after alkali metal reduction, focused on by dust removal installation; Aluminum oxide and impurity are fused to slag and float over molten iron surface, focus on to the desulphurization and slag skimming of steel-making work area by normal operation.
2. the method for high temperature iron bath process iron red mud according to claim 1, it is characterized in that, the main chemical compositions of described iron red mud is: Fe
2o
3be 30 ~ 70wt%, Al
2o
3be 5 ~ 30wt%, Na
2o is 0 ~ 10wt%, and all the other are SiO
2, CaO and other impurity.
3. the method for high temperature iron bath process iron red mud according to claim 1, it is characterized in that, described carbon raw material is coal dust or coke powder, and its fixed carbon content is greater than 70wt%, and sulphur content is less than 1wt%.
4. the method for high temperature iron bath process iron red mud according to claim 1, it is characterized in that, described additive is Fluorspar Powder, its CaF
2content>=85wt%.
5. the method for high temperature iron bath process iron red mud according to claim 1, it is characterized in that, the feed postition of described red mud agglomerate for join in molten iron stream from trough, swinging flow jet continuous uniform, or joins in iron ladle slack tank in advance, and then loads molten iron.
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| JP6460531B2 (en) * | 2015-05-28 | 2019-01-30 | 株式会社神戸製鋼所 | Method for producing reduced iron |
| CN106868241A (en) * | 2015-12-11 | 2017-06-20 | 北京亿玮坤节能科技有限公司 | Steel-making, ironmaking dedusting ash solid waste recovery system and its recovery method |
| CN107287367B (en) * | 2016-03-31 | 2019-04-26 | 鞍钢股份有限公司 | Method for recovering iron by utilizing high-iron red mud |
| CN107988458A (en) * | 2017-12-18 | 2018-05-04 | 莱芜市东冶新材料有限公司 | A kind of steel-making refining desulfuration agent based on red mud modification melting and preparation method thereof |
| CN109913604B (en) * | 2019-04-11 | 2021-02-26 | 东北大学 | Method for extracting iron from high-iron red mud and directly cementing |
| CN110157902A (en) * | 2019-05-27 | 2019-08-23 | 东北大学 | A kind of method of red mud resource utilization in molten iron pretreatment |
| CN114657303B (en) * | 2022-05-24 | 2022-08-16 | 山西建龙实业有限公司 | Method for synergistically utilizing high-iron red mud and scrap steel |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2596003B2 (en) * | 1987-10-15 | 1997-04-02 | 日本鋼管株式会社 | Smelting reduction method |
| CN102583477A (en) * | 2012-03-16 | 2012-07-18 | 东北大学 | Comprehensive utilization method of high-ferrum and low-grade bauxite |
| CN102732662A (en) * | 2012-06-02 | 2012-10-17 | 胡长春 | Slag-free production process using bauxite or red mud |
| CN102816880A (en) * | 2012-08-17 | 2012-12-12 | 东北大学 | Ironmaking and aluminum extraction comprehensive utilization method of high-iron red mud |
| CN102839249A (en) * | 2012-08-03 | 2012-12-26 | 莱芜钢铁集团有限公司 | Method for producing iron fine powder by directly reducing high-iron red mud with rotary hearth furnace |
| CN102851425A (en) * | 2012-08-17 | 2013-01-02 | 东北大学 | Method for high-efficiency separation and comprehensive utilization of iron, aluminum and sodium in high-iron red mud |
-
2013
- 2013-09-06 CN CN201310402154.9A patent/CN103468848B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2596003B2 (en) * | 1987-10-15 | 1997-04-02 | 日本鋼管株式会社 | Smelting reduction method |
| CN102583477A (en) * | 2012-03-16 | 2012-07-18 | 东北大学 | Comprehensive utilization method of high-ferrum and low-grade bauxite |
| CN102732662A (en) * | 2012-06-02 | 2012-10-17 | 胡长春 | Slag-free production process using bauxite or red mud |
| CN102839249A (en) * | 2012-08-03 | 2012-12-26 | 莱芜钢铁集团有限公司 | Method for producing iron fine powder by directly reducing high-iron red mud with rotary hearth furnace |
| CN102816880A (en) * | 2012-08-17 | 2012-12-12 | 东北大学 | Ironmaking and aluminum extraction comprehensive utilization method of high-iron red mud |
| CN102851425A (en) * | 2012-08-17 | 2013-01-02 | 东北大学 | Method for high-efficiency separation and comprehensive utilization of iron, aluminum and sodium in high-iron red mud |
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